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Updated: Jun 28, 2026

Process Optimization using High Throughput Automated Micro-Bioreactors in Chinese Hamster Ovary Cell Cultivation
Published on: May 18, 2020
Performance analyses of a pH-shift and DOT-shift integrated fed-batch fermentation process for the production of
Ya-Jie Tang1, Wei Zhang, Jian-Jiang Zhong
1Hubei Provincial Key Laboratory of Industrial Microbiology, College of Bioengineering, Hubei University of Technology, Wuhan, China. yajietang@hotmail.com
Abstract:
Investigations on Ganoderma lucidum fermentation suggested that the responses of the cell growth and metabolites biosynthesis to pH and dissolved oxygen tension (DOT) were different. The ganoderic acid (GA) production of 321.6 mg/L was obtained in the pH-shift culture by combining a 4-day culture at pH 3.0 with the following 6-day culture at pH 4.5, which was higher by 45% and 300% compared with the culture at pH 3.0 and 4.5, respectively. The GA production of 487.1mg/L was achieved in the DOT-shift culture by combining a 6-day culture at 25% of DOT with a following 6-day culture at 10% of DOT, which was higher by 43% and 230% compared with the culture at 25% and 10% of DOT, respectively. A fed-batch fermentation process by combining the above-mentioned pH-shift and DOT-shift strategies resulted in a significant synergistic enhancement of GA accumulation up to 754.6 mg/L, which is the highest reported in the submerged fermentation of G. lucidum in stirred-tank bioreactor.
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